CN111628199A - Sectional type fuel cell anchor clamps - Google Patents
Sectional type fuel cell anchor clamps Download PDFInfo
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- CN111628199A CN111628199A CN202010473088.4A CN202010473088A CN111628199A CN 111628199 A CN111628199 A CN 111628199A CN 202010473088 A CN202010473088 A CN 202010473088A CN 111628199 A CN111628199 A CN 111628199A
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- bipolar plate
- bipolar
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- 239000000446 fuel Substances 0.000 title claims abstract description 41
- 239000012528 membrane Substances 0.000 claims abstract description 35
- 238000010438 heat treatment Methods 0.000 claims abstract description 29
- 238000007789 sealing Methods 0.000 claims description 15
- 238000001816 cooling Methods 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 6
- 238000009529 body temperature measurement Methods 0.000 claims description 5
- 229920000515 polycarbonate Polymers 0.000 claims description 4
- 239000004417 polycarbonate Substances 0.000 claims description 4
- 239000003054 catalyst Substances 0.000 abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 230000002277 temperature effect Effects 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
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Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1004—Fuel cells with solid electrolytes characterised by membrane-electrode assemblies [MEA]
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0258—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
- H01M8/0276—Sealing means characterised by their form
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1007—Fuel cells with solid electrolytes with both reactants being gaseous or vaporised
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
Abstract
The invention provides a sectional type fuel cell clamp, which comprises a cathode end, a membrane electrode and an anode end, wherein the cathode end is provided with a plurality of through holes; the cathode end and the anode end are of symmetrical structures; the cathode end comprises a cathode flow passage plate frame and a cathode bipolar plate, and the cathode bipolar plate is correspondingly arranged in a plurality of hole positions on the cathode flow passage plate frame. Cathode flow channels are respectively arranged on the surface of one side of the cathode bipolar plate, and a plurality of cathode collector plates are arranged on the other side of the cathode bipolar plate. And one side of the cathode collector plates is sequentially provided with a cathode heating plate and a cathode radiating fin. The cathode flow channel plate frame is respectively provided with a plurality of cathode current collecting holes and a plurality of cathode temperature measuring holes. The cathode terminal and the anode terminal have the same structure. Through the mode, more accurate temperature control of different cathode bipolar plates and anode bipolar plates is realized, the invention not only can be suitable for membrane electrode with gradient catalyst concentration in a plane, but also can realize temperature gradient setting, and can be better applied to experimental research.
Description
Technical Field
The invention belongs to the field of fuel cells, and particularly relates to a sectional type fuel cell clamp.
Background
Fuel cells have become a promising power fixture due to their advantages of zero emissions, long endurance, and high energy conversion efficiency, but the durability of their components and the high cost of materials have been the direction to be further improved. The reactant concentration distribution on the membrane electrode is fanned in the direction of the parallel flow channel inlet and outlet of the fuel cell. The current density on the membrane electrode is not uniform due to the inconsistent mass transfer rate on the uniformly distributed catalytic layer caused by the mismatch of the mass transfer rate and the reaction rate. As the reaction proceeds, the amount of cathode water produced is also affected by the non-uniform current density, which is very likely to cause flooding in some areas. The distribution of the catalyst can affect the difference in water content at different locations. In addition, the saturated vapor pressure of water changes along with the change of temperature, and the uniform temperature rising mode of the fuel cell ensures that the relative humidity inside the flow channel cannot reach 100% at the same time, thereby influencing the concentration of liquid water in the porous electrode.
The uniform catalyst distribution not only cannot be reasonably utilized but also results in an increase in the cost of the membrane electrode. A single heating temperature also tends to cause inconsistencies in the water content of the film. The above are two problems in terms of high cost and durability of the fuel cell.
Traditional laboratory fuel cell fixtures are dominated by single cells and stacks. The monocell has a fine and small flow channel structure, is generally used for researching the characteristics of the membrane electrode, such as catalyst materials, loading capacity and operation condition control, and has a relatively accurate and reliable data result. Compared with single cells, the data measured by the stack has more practical application value, but the experimental cost of the fuel cell stack using a large number of membrane electrodes is very high. The research of the gradient distribution and gradient temperature of the catalyst used for the fuel cell clamp by the existing single cell and the electric pile has certain limitations.
Disclosure of Invention
The invention aims to provide a sectional type fuel cell clamp, which is suitable for a membrane electrode with gradient catalyst concentration in a plane, can realize temperature gradient arrangement and can be better applied to experimental research.
The technical scheme of the invention is as follows: a sectional type fuel cell clamp comprises a cathode end, a membrane electrode and an anode end; the cathode end and the anode end are of symmetrical structures and are symmetrically arranged on two sides of the membrane electrode;
a cathode gasket is arranged between the cathode end and the membrane electrode; an anode gasket is arranged between the anode end and the membrane electrode;
the cathode end comprises a cathode flow channel plate frame and a cathode bipolar plate; a plurality of through hole sites are formed on the cathode flow channel plate frame; the cathode bipolar plate comprises a cathode gas inlet end bipolar plate, a plurality of cathode middle section bipolar plates and a cathode gas outlet end bipolar plate; the cathode bipolar plate is correspondingly arranged in a hole position on the cathode flow channel plate frame;
the anode end comprises an anode runner plate frame and an anode bipolar plate; the anode runner plate frame is provided with a plurality of through hole sites; the anode bipolar plate comprises an anode gas inlet end bipolar plate, a plurality of anode middle section bipolar plates and an anode gas outlet end bipolar plate; the anode bipolar plate is correspondingly arranged in a hole position on the anode flow channel plate frame;
the surface of the cathode bipolar plate, which is positioned at one side of the membrane electrode, is provided with a cathode flow channel, and the other side of the cathode bipolar plate is provided with a plurality of cathode collector plates;
the surface of the anode bipolar plate, which is positioned at one side of the membrane electrode, is provided with an anode flow channel, and the other side of the anode bipolar plate is provided with a plurality of anode current collecting plates;
the air inlet end of the bipolar plate at the cathode air inlet end is provided with a cathode air inlet, and the cathode air inlet is communicated with a cathode flow passage on the bipolar plate at the cathode air inlet end; the gas outlet end of the cathode gas outlet end bipolar plate is provided with a cathode gas outlet hole which is communicated with a cathode flow channel on the cathode gas outlet end bipolar plate;
an anode air inlet is formed in the air inlet end of the anode air inlet end bipolar plate and is communicated with an anode flow passage on the anode air inlet end bipolar plate; the gas outlet end of the anode gas outlet end bipolar plate is provided with an anode gas outlet hole, and the anode gas outlet hole is communicated with a cathode flow channel on the anode gas outlet end bipolar plate.
In the above scheme, the surface of the cathode runner plate frame on one side of the cathode gasket is provided with a cathode runner plate sealing groove; the sealing groove of the cathode runner plate is provided with a cathode runner plate air-tight gasket;
the surface of the anode runner plate frame, which is positioned on one side of the anode gasket, is provided with an anode runner plate sealing groove; and an anode runner plate airtight pad is arranged on the sealing groove of the anode runner plate.
In the scheme, one side of the cathode collector plates is provided with a cathode heating sheet; and one side of the anode collector plates is provided with an anode heating sheet.
Furthermore, cathode cooling fins are arranged on one side of the cathode heating fins; and one side of the anode heating plates is provided with an anode radiating fin.
Further, the device also comprises a cathode end plate and an anode end plate; the cathode end plate is provided with a groove position and a through hole, and a cathode heating plate and a cathode radiating fin are respectively arranged on the groove position and the through hole; the anode end plate is provided with a groove position and a through hole, and an anode heating plate and an anode radiating fin are respectively installed on the groove position and the through hole.
In the above scheme, the cathode radiating fins and the anode radiating fins are fin radiators.
In the above scheme, the cathode end plate and the anode end plate are made of polycarbonate materials.
In the above scheme, the cathode flow channel plate frame is provided with a plurality of cathode current collecting holes corresponding to the cathode bipolar plate; a plurality of cathode current collecting holes are provided with cathode current collecting columns; a plurality of cathode current collecting columns are connected with the cathode bipolar plate;
the anode flow passage plate frame is provided with a plurality of anode current collecting holes corresponding to the anode bipolar plate; the anode current collecting holes are provided with anode current collecting columns; a plurality of the anode collector columns 33 are connected to the anode bipolar plate.
In the above scheme, the cathode flow channel plate frame is provided with a plurality of cathode temperature measurement holes corresponding to the cathode bipolar plate; the anode runner plate frame is provided with a plurality of anode temperature measuring holes corresponding to the anode bipolar plates.
Compared with the prior art, the invention has the beneficial effects that:
1. the invention provides a sectional type fuel cell clamp which comprises a cathode end, a membrane electrode and an anode end, wherein the cathode end and the anode end respectively comprise a cathode runner plate frame and an anode runner plate frame. The cathode flow passage plate frame and the anode flow passage plate frame are both provided with a plurality of through hole sites for mounting a plurality of cathode bipolar plates and a plurality of anode bipolar plates. The cathode flow passages between the cathode bipolar plates are communicated, and the anode flow passages between the anode bipolar plates are communicated. Different cathode bipolar plates and anode bipolar plates are correspondingly arranged at different positions of the membrane electrode. The catalyst concentration of the membrane electrode can be distributed in a gradient way, so that the membrane electrode is better utilized, the cost of the membrane electrode is reduced, and the durability of the fuel cell is improved.
2. The sectional type fuel cell clamp provided by the invention is provided with the cathode runner plate sealing groove and the cathode runner plate air-tight gasket, and the anode runner plate sealing groove and the anode runner plate air-tight gasket, so that the sealing property between the cathode runner plate frame and the cathode gasket can be ensured, and the sealing property between the anode runner plate frame and the anode gasket can be ensured
3. The segmented fuel cell clamp provided by the invention is also provided with a plurality of cathode heating sheets, anode heating sheets, a plurality of cathode radiating fins and anode radiating fins, so that more accurate temperature control of different cathode bipolar plates and anode bipolar plates is realized, the relative humidity inside a flow channel is ensured to be more uniform, and the performance stability of a fuel cell is improved.
4. The segmented fuel cell clamp provided by the invention further comprises a cathode end plate and an anode end plate, wherein the cathode end plate and the anode end plate are made of polycarbonate materials and are used for fixedly mounting a heating sheet and a radiating fin and avoiding the temperature influence between adjacent bipolar plates.
5. The segmented fuel cell clamp provided by the invention has the advantages that the cathode runner plate frame is provided with a plurality of cathode current collecting holes, and the anode runner plate frame is provided with a plurality of anode current collecting holes, so that electric signals generated on different bipolar plates can be conveniently measured. And a plurality of cathode temperature measuring holes and anode temperature measuring holes are formed, so that the temperature measurement of different bipolar plate positions can be realized. Through the mode, experimental research is better carried out on the fuel cell clamp.
Drawings
FIG. 1 is an overall axial view of a segmented fuel cell clamp according to the present invention;
FIG. 2 is an exploded view of the segmented fuel cell clamp of the present invention;
FIG. 3 is an enlarged view of the segmented fuel cell fixture cathode of the present invention;
FIG. 4 is a drawing of a segmented fuel cell clamp cathode end plate according to the present invention;
FIG. 5 is a diagram of a segmented fuel cell fixture cathode flow channel plate according to the present invention;
in the figure, 1, cathode terminal; 2. a membrane electrode; 3. an anode terminal; 4. a cathode pad; 5. an anode gasket; 6. a cathode flow field plate frame; 7. an anode flow channel plate frame; 8. a cathode inlet end bipolar plate; 9. a cathode middle section bipolar plate set; 10. a cathode gas outlet end bipolar plate; 11. an anode inlet end bipolar plate; 12. an anode middle section bipolar plate group; 13. an anode gas outlet end bipolar plate; 14. a cathode inlet hole; 15. a cathode gas outlet; 16. a cathode flow channel; 17. an anode inlet hole; 18. a cathode gas outlet; 19. an anode flow channel; 20. a cathode collector plate; 21. an anode current collector plate; 22. a cathode current collecting part; 23. an anode current collecting part; 24. a cathode end plate; 25. a cathode heating plate; (ii) a 26. An anode end plate; 27. an anode heating plate; 28. a cathode fin; 29. an anode heat sink; 30. a cathode collector; 31. an anode current collecting hole; 32. a cathode current collector column; 33. an anode current collector column; 34. a cathode temperature measurement hole; 35. an anode temperature measuring hole; 36. a cathode flow passage plate airtight pad; 37. a cathode runner plate seal groove; 38. an anode flow channel plate airtight pad; 39. an anode runner plate seal groove; 40. a screw; 41. positioning holes; 42. a nut;
Detailed Description
The present invention will be described in further detail with reference to the following detailed description of the drawings, but the scope of the present invention is not limited thereto.
1, 2, 3, 4 and 5, a segmented fuel cell fixture comprising a cathode end 1, a membrane electrode 2 and an anode end 3; the cathode end 1 and the anode end 3 are of symmetrical structures, the cathode end 1 and the anode end 3 are of the same structure, and the cathode end 1 and the anode end 3 are symmetrically arranged on two sides of the membrane electrode 2; the catalyst concentration on the membrane electrode 2 is distributed in a gradient manner.
A cathode gasket 4 is arranged between the cathode end 1 and the membrane electrode 2; an anode gasket 5 is arranged between the anode end 3 and the membrane electrode 2; the cathode gasket 4 and the anode gasket 5 are used to sandwich the membrane electrode 2.
The cathode terminal 1 comprises a cathode flow channel plate frame 6 and a cathode bipolar plate; the cathode flow channel plate frame 6 is provided with a plurality of through hole sites for installing cathode bipolar plates; the cathode bipolar plate comprises a cathode gas inlet end bipolar plate 8, a plurality of cathode middle section bipolar plates 9 and a cathode gas outlet end bipolar plate 10; the cathode bipolar plate is correspondingly arranged in a hole position on the cathode flow channel plate frame 6;
the anode end 3 comprises an anode flow channel plate frame 7 and an anode bipolar plate; the anode runner plate frame 7 is provided with a plurality of through hole sites for installing an anode bipolar plate; the anode bipolar plate comprises an anode gas inlet end bipolar plate 11, a plurality of anode middle section bipolar plates 12 and an anode gas outlet end bipolar plate 13; the anode bipolar plate is correspondingly arranged in a hole position on the anode flow channel plate frame 7;
preferably, the number of the upper hole sites of the cathode flow channel plate frame 6 and the anode flow channel plate frame 7 is 5.
The surface of the cathode bipolar plate at one side of the membrane electrode 2 is provided with a cathode flow channel 16, and the cathode flow channels 16 of different cathode bipolar plates are communicated.
The other side of the cathode bipolar plate is provided with a plurality of cathode current collecting plates 20 for collecting current on the cathode bipolar plate, the cathode current collecting plates 20 are connected with a cathode current collecting position 22 at the top, and the cathode current collecting position 22 is used for leading out the current generated by the cathode end 1.
The surface of the anode bipolar plate on one side of the membrane electrode 2 is provided with an anode flow channel 19, and the cathode flow channels 19 of different anode bipolar plates are communicated.
The other side of the anode bipolar plate is provided with a plurality of anode current collecting plates 21 for collecting current on the anode bipolar plate, the anode current collecting plates 21 are connected with an anode current collecting part 23 at the top, and the anode current collecting part 23 is used for leading out the current generated by the anode end 3.
Preferably, the cathode flow channels 16 and the anode flow channels 19 are both parallel flow channels.
A cathode air inlet 14 is arranged on the air inlet end of the cathode air inlet end bipolar plate 8, and the cathode air inlet 14 is communicated with a cathode flow channel 16 on the cathode air inlet end bipolar plate 8; the gas outlet end of the cathode gas outlet end bipolar plate 10 is provided with a cathode gas outlet hole 15, and the cathode gas outlet hole 15 is communicated with a cathode flow channel 16 on the cathode gas outlet end bipolar plate 10; after the cathode gas is introduced, the cathode gas passes through the cathode gas inlet hole 14, the cathode flow channel 16 and the cathode gas outlet hole 15 in sequence.
An anode air inlet 17 is arranged on the air inlet end of the anode air inlet end bipolar plate 11, and the anode air inlet 17 is communicated with an anode flow channel 19 on the anode air inlet end bipolar plate 11; the gas outlet end of the anode gas outlet end bipolar plate 13 is provided with an anode gas outlet hole 18, and the anode gas outlet hole 18 is communicated with an anode flow channel 19 on the anode gas outlet end bipolar plate 13; after the anode gas is introduced, the anode gas passes through the anode gas inlet hole 17, the anode flow channel 19 and the anode gas outlet hole 18 in sequence.
The surface of the cathode runner plate frame 6, which is positioned at one side of the cathode gasket 4, is provided with a cathode runner plate sealing groove 37; the cathode runner plate sealing groove 37 is provided with a cathode runner plate airtight gasket 36 for ensuring airtightness of the cathode terminal 1.
The surface of the anode runner plate frame 7, which is positioned on one side of the anode gasket 5, is provided with an anode runner plate sealing groove 39; the anode runner plate sealing groove 39 is provided with an anode runner plate air-tight gasket 38 for ensuring air-tightness of the cathode terminal 3.
The cathode end 1 and the anode end 3 are provided with a plurality of positioning holes 41, and the whole sectional type fuel cell clamp is fixed by a plurality of screws 40 and nuts 42.
A cathode end plate 24 and an anode end plate 26; one side of the cathode collector plates 20 is provided with cathode heating sheets 25 for independently heating different cathode bipolar plates; one side of the anode collector plates 21 is provided with an anode heating sheet 27 for independently heating different anode bipolar plates;
one side of the cathode heating plates 25 is provided with a cathode cooling fin 28 for cooling different cathode bipolar plates; one side of the anode heating sheets 27 is provided with an anode cooling fin 29 for cooling different anode bipolar plates;
the cathode end plate 24 is provided with a groove position and a through hole, and the cathode heating plate 25 and the cathode radiating fin 28 are respectively installed to realize the fixed installation of the cathode heating plate 25 and the cathode radiating fin 28; the anode end plate 26 is provided with a groove and a through hole, and the anode heating plate 27 and the anode radiating fin 29 are respectively installed on the groove and the through hole, so that the anode heating plate 27 and the anode radiating fin 29 are fixedly installed.
Through the mode, the more accurate temperature control of different cathode bipolar plates and anode bipolar plates is realized, the relative humidity inside the flow channel is ensured to be more uniform, and the performance stability of the fuel cell is improved.
Preferably, the cathode cooling fin 28 and the anode cooling fin 29 are fin radiators, so that a better heat dissipation effect is achieved.
Preferably, the cathode end plate 24 and the anode end plate 26 are polycarbonate material to avoid temperature effects between adjacent bipolar plates.
The cathode flow channel plate frame 6 is provided with a plurality of cathode current collecting holes 30 corresponding to the cathode bipolar plate; a plurality of cathode current collecting holes 30 are provided with cathode current collecting columns 32; a plurality of cathode collector columns 32 are connected to the cathode bipolar plate; a plurality of anode collecting holes 31 corresponding to the anode bipolar plates are arranged on the anode flow channel plate frame 7; the anode current collecting columns 33 are arranged on the plurality of anode current collecting holes 31; a plurality of the anode collector columns 33 are connected to the anode bipolar plate. Through the mode, the electric signals generated on different bipolar plates can be conveniently measured.
The cathode flow channel plate frame 6 is provided with a plurality of cathode temperature measuring holes 34 corresponding to the cathode bipolar plate, the anode flow channel plate frame 7 is provided with a plurality of anode temperature measuring holes 35 corresponding to the anode bipolar plate, and a thermocouple can be inserted through the cathode temperature measuring holes 34 and the anode temperature measuring holes 35 to realize temperature measurement of different bipolar plate positions.
The segmented fuel cell fixture can adopt two ventilation modes of parallel flow and convection, namely the air inlet directions of the cathode end and the anode end are the same or opposite.
The sectional fuel cell clamp has two electric signal reading modes, and an external electrode clamp 22, a cathode current collecting position 23 and an anode current collecting position are arranged when the overall performance of the cell is read; when the local battery performance is tested, the external electrodes are clamped on any pair of the cathode current collecting columns 32 and the anode current collecting columns 33 according to requirements.
Through the mode, the device not only can be suitable for the membrane electrode with the gradient catalyst concentration in the plane, but also can realize the temperature gradient arrangement, and can be better applied to experimental research.
It should be understood that although the present invention has been described in terms of various embodiments, not every embodiment includes only a single embodiment, and such description is for clarity purposes only, and those skilled in the art will recognize that the embodiments described herein can be combined as a whole to form other embodiments as would be understood by those skilled in the art.
The above detailed description is given for the purpose of illustrating a practical embodiment of the present invention and is not to be construed as limiting the scope of the present invention, and any equivalent embodiments or modifications thereof without departing from the technical spirit of the present invention are included in the scope of the present invention.
Claims (9)
1. A sectional type fuel cell clamp is characterized by comprising a cathode end (1), a membrane electrode (2) and an anode end (3); the cathode end (1) and the anode end (3) are of symmetrical structures, and the cathode end (1) and the anode end (3) are symmetrically arranged on two sides of the membrane electrode (2);
a cathode gasket (4) is arranged between the cathode end (1) and the membrane electrode (2); an anode gasket (5) is arranged between the anode end (3) and the membrane electrode (2);
the cathode end (1) comprises a cathode flow channel plate frame (6) and a cathode bipolar plate; a plurality of through hole sites are formed on the cathode flow channel plate frame (6); the cathode bipolar plate comprises a cathode gas inlet end bipolar plate (8), a plurality of cathode middle section bipolar plates (9) and a cathode gas outlet end bipolar plate (10); the cathode bipolar plate is correspondingly arranged in a hole position on the cathode flow channel plate frame (6);
the anode end (3) comprises an anode runner plate frame (7) and an anode bipolar plate; a plurality of through hole sites are formed on the anode runner plate frame (7); the anode bipolar plate comprises an anode gas inlet end bipolar plate (11), a plurality of anode middle section bipolar plates (12) and an anode gas outlet end bipolar plate (13); the anode bipolar plate is correspondingly arranged in a hole position on the anode runner plate frame (7);
a cathode flow channel (16) is arranged on the surface of the cathode bipolar plate on one side of the membrane electrode (2), and a plurality of cathode collector plates (20) are arranged on the other side of the cathode bipolar plate;
an anode flow channel (19) is arranged on the surface of the anode bipolar plate on one side of the membrane electrode (2), and a plurality of anode current collecting plates (21) are arranged on the other side of the anode bipolar plate;
a cathode air inlet (14) is formed in the air inlet end of the cathode air inlet end bipolar plate (8), and the cathode air inlet (14) is communicated with a cathode flow channel (16) on the cathode air inlet end bipolar plate (8); a cathode gas outlet hole (15) is formed in the gas outlet end of the cathode gas outlet end bipolar plate (10), and the cathode gas outlet hole (15) is communicated with a cathode flow channel (16) on the cathode gas outlet end bipolar plate (10);
an anode air inlet (17) is formed in the air inlet end of the anode air inlet end bipolar plate (11), and the anode air inlet (17) is communicated with an anode flow channel (19) on the anode air inlet end bipolar plate (11); an anode gas outlet hole (18) is formed in the gas outlet end of the anode gas outlet end bipolar plate (13), and the anode gas outlet hole (18) is communicated with a cathode flow channel (19) on the anode gas outlet end bipolar plate (13).
2. The segmented fuel cell clamp of claim 1, wherein the surface of the cathode flow channel plate frame (6) on the side of the cathode gasket (4) is provided with a cathode flow channel plate seal groove (37); a cathode flow channel plate airtight pad (36) is arranged on the cathode flow channel plate sealing groove (37);
an anode runner plate sealing groove (39) is formed in the surface, located on one side of the anode gasket (5), of the anode runner plate frame (7); and an anode flow channel plate airtight pad (38) is arranged on the anode flow channel plate sealing groove (39).
3. The segmented fuel cell fixture of claim 1, wherein one side of a number of said cathode collector plates (20) is provided with cathode heating fins (25); an anode heating sheet (27) is arranged on one side of the anode collector plates (21).
4. The segmented fuel cell clamp of claim 3, wherein a number of said cathode heating plates (25) are provided with cathode cooling fins (28) on one side; and one side of the anode heating sheets (27) is provided with an anode radiating sheet (29).
5. The segmented fuel cell clamp of claim 4, further comprising a cathode end plate (24) and an anode end plate (26); the cathode end plate (24) is provided with a groove position and a through hole which are respectively provided with a cathode heating plate (25) and a cathode radiating fin (28); the anode end plate (26) is provided with a groove and a through hole, and an anode heating sheet (27) and an anode cooling sheet (29) are respectively arranged on the groove and the through hole.
6. The segmented fuel cell clamp of claim 4, wherein the cathode and anode fins (28, 29) are finned heat sinks.
7. The segmented fuel cell clamp of claim 5, wherein the cathode end plate (24) and anode end plate (26) are polycarbonate materials.
8. The segmented fuel cell fixture of claim 1, wherein the cathode flow field plate frame (6) has a plurality of cathode manifolds (30) corresponding to the cathode bipolar plates; a plurality of cathode current collecting holes (30) are provided with cathode current collecting columns (32); a plurality of cathode collector columns (32) are connected with the cathode bipolar plate;
a plurality of anode flow collecting holes (31) corresponding to the anode bipolar plate are formed in the anode flow channel plate frame (7); the anode current collecting holes (31) are provided with anode current collecting columns (33); a plurality of the anode current collecting columns (33) are connected with the anode bipolar plate.
9. The segmented fuel cell fixture of claim 1, wherein the cathode flow channel plate frame (6) is provided with a plurality of cathode temperature measurement holes (34) corresponding to the cathode bipolar plates; the anode runner plate frame (7) is provided with a plurality of anode temperature measuring holes (35) corresponding to the anode bipolar plate.
Priority Applications (1)
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CN202010473088.4A CN111628199B (en) | 2020-05-29 | 2020-05-29 | Sectional type fuel cell fixture |
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CN202010473088.4A CN111628199B (en) | 2020-05-29 | 2020-05-29 | Sectional type fuel cell fixture |
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CN111628199B CN111628199B (en) | 2024-04-09 |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113793944A (en) * | 2021-08-03 | 2021-12-14 | 广东电网有限责任公司广州供电局 | Fuel cell clamp and testing device |
CN114935951A (en) * | 2022-04-08 | 2022-08-23 | 山东国创燃料电池技术创新中心有限公司 | Temperature control method for fuel cell test fixture |
CN116111147A (en) * | 2023-04-13 | 2023-05-12 | 北京新研创能科技有限公司 | Temperature management method and system for hydrogen fuel cell |
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CN116111147A (en) * | 2023-04-13 | 2023-05-12 | 北京新研创能科技有限公司 | Temperature management method and system for hydrogen fuel cell |
CN116111147B (en) * | 2023-04-13 | 2023-06-30 | 北京新研创能科技有限公司 | Temperature management method and system for hydrogen fuel cell |
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